CN101293706A - Multi-stage inner circulation anaerobic reactor - Google Patents
Multi-stage inner circulation anaerobic reactor Download PDFInfo
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- CN101293706A CN101293706A CNA2008100696991A CN200810069699A CN101293706A CN 101293706 A CN101293706 A CN 101293706A CN A2008100696991 A CNA2008100696991 A CN A2008100696991A CN 200810069699 A CN200810069699 A CN 200810069699A CN 101293706 A CN101293706 A CN 101293706A
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- gas
- liquid separator
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- anaerobic
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
The invention relates to a multi-stage internal circular anaerobic reactor which aims at solving the defects of existing anaerobic reactors, such as difficulty in separating the sludge and hydraulic retention time, long treatment period, high solid-containing content of effluent, and limit to the treatment of organic wastewater with medium and high temperature and high concentration. The anaerobic reaction zone of the reactor is arranged above three stages, each of which is provided with a riser pipe used for leading fluid to flow up to a gas-liquid separator at the top part through an air collection baffle-board, a recirculatory pipe used for leading the fluid to flow down to a solid-liquid separator at the bottom part and a water distributor used for leading the fluid to enter the anaerobic reaction zone to carry out fluid circulation. The reactor is easy to operate and manage, optimizes disposition conditions and improves biomass in the reactor. The full contact of wastewater and microbe strengthens the mass transfer between the wastewater and particle sludge and guarantees the normal operation of the reactor in larger volume load.
Description
Technical field
The present invention relates to biological chemistry environment-friendly type engineering, particularly a kind of multi-stage inner circulation anaerobic reactor.
Background technology
The Development Of Anaerobic Reactor course can be divided into three typical stages: the fs is representative with continuously stirring formula (CSTR), shortcoming: mud is difficult to separate with hydraulic detention time, long processing period, water outlet solid content height; Subordinate phase is representative with upflow anaerobic sludge blanket process (UASB), than first-generation reactor excellence, but is only limited to high temperature and high concentrated organic wastewater in the processing; Phase III is representative with expanded granular sludge bed (ECSB) and inner circulation reactor (IC), has further improved the performance of reactor, but imperfect.
Summary of the invention
The present invention is directed to above-mentioned deficiency, combine each relative merits for reactor, therefrom learn from other's strong points to offset one's weaknesses, the reactor superposition series connection with most characteristic makes it to become holistic multi-stage inner circulation anaerobic reactor.
The present invention is achieved through technology:
A kind of multi-stage inner circulation anaerobic reactor, the anaerobic reaction district is provided with more than three grades, upspout, return line, the mistake gas collection reflectors all established at different levels; Be provided with gas-liquid separator at top, anaerobic reaction district, the up-flow gas-liquid is after the gas-liquid separation of top, the pipeline that biogas is provided with from the top is drawn, feed liquid is fallen the solid-liquid separator and water inlet thorough mixing that flow to the bottom by the return line of each reaction zone, thereby cross water distributor and enter the circulation of anaerobic reaction district realization fluid, until top, the plug-flow that makes progress is gradually finished whole anaerobic reaction processes to mixed solution from end level.
For better effect: the water distributor structure is that water distribution board is with 45 ° 6～12 water inlet pipes to be installed on a whole flat board, and an opening is established at the center of water distribution board.
Valve, water inlet pipe connect solid-liquid separator, solid-liquid separator connects water distribution board, water distribution board connects first reaction zone, first reacted the gas collection reflector connects second reaction zone, each reaction zone is crossed the gas collection reflector and is connected next reaction zone to the superiors' reaction zone, the superiors' reaction zone is crossed the gas collection reflector and is connected the settling region, and the settling region connects effluent trough and gas-liquid separator respectively.
Solid-liquid separator is conical.
Gas-liquid separator is formed full circle shape at continuous bay wall.
Gas-liquid separator is two semicircles, half connects odd number reaction zone upspout and return line, second half connects even number reaction zone upspout, after the up-flow gas-liquid of each reactor enters gas-liquid separator, biogas is from the pipe connection of continuing to use of separator two halves, draw with valve switch control, and gas meter is set; Up-flow liquid is continued to use pipeline and is communicated with under the two halves separator, return line connects solid-liquid separator.
The present invention gets the excellent weak point of keeping away to prior art and structurally simplifies, and manage with easy handling: water inlet is controlled with valve, and water distribution is evenly distributed, and reaction zone is established multistage, the upspouts of all establishing at different levels.Be provided with gas-liquid separator at the top, the up-flow gas-liquid is after the gas-liquid separation of top, and biogas is drawn, after feed liquid is fallen the solid-liquid separator that flow to the bottom by return line,, cross water distributor and enter the anaerobic reaction district with the water inlet thorough mixing, strengthen upflow velocity, thereby realized bigger fluid circulation.The gas of reactor reduces from the bottom to top step by step.Because the load of last step is low, settling condition is optimized, thereby the biomass of reactor significantly improves.Sewage and microorganism full contact have been strengthened the mass transfer between sewage and granule sludge, have guaranteed reactor normally operation under big volumetric loading.Pretreated waste water enters solid-liquid separator through valve control, and in separator: heavy solids compiles the heart channel of Hang-Shaoyin pipeline and valve control discharge in the conical bottom under the circumference flow action; Easily degraded and suspended matter are crossed the water distribution board inclined tube and are entered a reaction zone, mix with mud and to contact, the micro bubbles that produces is in uphill process, and constantly merging forms gradually than air pocket, runs into the gas collection reflector, be folded to a reaction zone upspout, up-flow is to the top gas-liquid separator, and biogas is separated draws, and feed liquid is fallen the solid-liquid separator that flow to the bottom and mixed with water inlet from return line, enter a reaction zone after water distribution board, constantly circulation has strengthened upflow velocity.Second to the five later reaction zone repeats the first reaction zone process separately, just flow reduces gradually, and load progressively reduces, and settling condition is optimized gradually, thereby the biomass of reactor is significantly improved, for the high-level efficiency height of sewage disposal goes the rate of falling to lay a good foundation.Sewage is through behind a plurality of reaction zones, because disturbance is little, and particulate matter easily flows in the reaction zone, clear liquid is just discharged from the effluent trough of upper end and entered reprocessing facility in the settling region.
For better effect, solid-liquid separator is designed to taper shape, so that water inlet and recirculation water promote the water body directed flow under action of gravity; Heavy solids compiles bottom centre, discharges by pipeline and valve control; Easily degradation product and suspended matter are crossed the water distribution board inclined tube and are evenly entered anaerobism one reaction zone, and later reaction process is boosted step by step.Gas-liquid separator also is designed to circle.And draw biogas with pipe connection in the top of gas-liquid separator, followingly use the pipe connection feed liquid, so that liquid return.Load onto gas meter, be convenient to monitor control; Water distribution board is that a whole dull and stereotyped water inlet pipe of installing with 45 of going up can be realized evenly water inlet.The opening that its center is provided with can play buffering and fluidised form regulating effect to reactor.
This reactor can independent operating, more can a plurality of combined runnings in parallel.Its bay wall is used steel reinforcing during independent operating, to bear big pressure; During a plurality of combined running in parallel, only the bay wall on surrounding edge edge is reinforced, all bay walls of intermediate zone are built by laying bricks or stones with the common building material and are got final product, and can save construction investment.The design scope of application is extensive like this: enterprises and institutions and sewage work all can apply in a flexible way.For example: single reactor useful volume 340m
3,, be combined into sewage works thousands of, tens thousand of, hundreds thousand of cubic metres with many ponds and all be easy to if hydraulic detention time is 8 hours.And can make the sewage work of energy-conservation, production capacity, complete ecology, recycling economy, full environment-friendly type, for society benefits for the centuries for human.
Description of drawings
Fig. 1 is the present invention's one Pyatyi internal-circulation anaerobic reactor structural representation orthographic plan.
Fig. 2 is the sectional view of Fig. 1.
Fig. 3 is the water distributor structural representation.
Fig. 4 is the water inlet pipe cross-sectional view of water distribution board
Embodiment
Embodiment one
See Fig. 2, pretreated waste water enters water inlet pipe 7 through valve 93 controls and connects solid-liquid separator 70, and solid-liquid separator 70 is conical; Heavy solids compile solid-liquid separator at 70 the end 93 controls of the heart channel of Hang-Shaoyin pipeline 9 and valve discharge otherwise processed, easy degradation product is crossed water distribution board 91 with suspended matter and is connected a reaction zone 10 with water distribution inclined tube 92, one reaction zone 10 is crossed gas collection reflector 90 and is connected two reaction zones 20, two reaction zones 20 are crossed gas collection reflector 90 and are connected three reaction zones 30, three reactions many 30 are crossed gas collection reflector 90 and are connected four reaction zones 40, four reaction zones 40 are crossed gas collection reflector 90 and are connected five reaction zones 50, five reaction zones 50 are crossed gas collection reflector 90 and are connected settling region 60, the mud of settling region 60 is in gas collection reflector 90 passes back into the anaerobic reaction district, clear liquid is discharged by the effluent trough 8 on top, enters reprocessing facility.
See Fig. 1, the gas-liquid entering part upspout separately that each reaction zone produces.Arrange on upspout branch both sides: one, the up-flow of three, five reaction zones management 1,3,5 comes in left half separator, and the upspout 2,4 of two, four reaction zones comes in right half separator, after the gas-liquid separation of two semicircle gas-liquid separators 80; With pipeline 9 biogas is communicated with, draws, load onto gas meter 94, to monitor running condition with valve switch 93 controls; With pipeline 61 feed liquid is communicated with, falls through return line 6 and flow in the solid-liquid separator 70, and enter in the reactor again after water inlet mixes, thereby realize that fluid circulates.Water distribution board 91 is that whole dull and stereotyped going up with 45 installed evenly water inlet of 8 water inlet pipes, 92 realizations.The center of water distribution board 91 is established 95 pairs of reactors of opening and is played buffering and fluidised form regulating effect.
This reactor list pond useful volume 340m
3(or 130m
3), pond combined running in parallel can or be counted with single pond by general enterprises and institutions.During in parallel combined running, it is sharing body that 3/4ths bay wall is arranged approximately, can reduce investment outlay, and its stable security is stronger.If hydraulic detention time is 8 hours, for the sewage work of specialty, available ten ponds or tens of pond combined running in parallel.Day disposes of sewage and can set up into ten thousand m
3, tens thousand of m
3And even hundreds thousand of m
3Sewage work.Form that loopful is protected, recycling economy, energy-conservation, the production capacity of Sustainable development, complete ecological, type of production enterprise that benefit is stable.
Claims (6)
1, a kind of multi-stage inner circulation anaerobic reactor comprises valve, pipeline, it is characterized in that: the anaerobic reaction district is provided with more than three grades, upspout, mistake gas collection reflector (90), the return lines (6) all established at different levels; Be provided with gas-liquid separator (80) at top, anaerobic reaction district, the up-flow gas-liquid is after the gas-liquid separation of top, the pipeline (9) that biogas is provided with from the top is drawn, feed liquid is fallen the solid-liquid separator (70) and water inlet thorough mixing that flow to the bottom by the return line (6) of each reaction zone, thereby cross water distributor and enter the circulation of anaerobic reaction district realization fluid, until top, the plug-flow that makes progress is gradually finished whole anaerobic reaction processes to mixed solution from end level.
2, multi-stage inner circulation anaerobic reactor as claimed in claim 1 is characterized in that: the water distributor structure is that water distribution board (91) is with 45 6～12 water inlet pipes (92) to be installed on a whole flat board, and an opening (95) is established at the center of water distribution board (91).
3, a kind of multi-stage inner circulation anaerobic reactor as claimed in claim 1, it is characterized in that: valve (93), water inlet pipe (7) connects solid-liquid separator (70), solid-liquid separator (70) connects water distribution board (91), water distribution board (91) connects first reaction zone (10), first reaction (10) is crossed gas collection reflector (90) and is connected second reaction zone (20), each reaction zone is crossed gas collection reflector (90) and is connected next reaction zone to the superiors' reaction zone, the superiors' reaction zone is crossed gas collection reflector (90) and is connected settling region (60), and settling region (60) connect effluent trough (8) and gas-liquid separator (80) respectively.
4, as claim 1 or 3 described multi-stage inner circulation anaerobic reactors, it is characterized in that: solid-liquid separator (70) is for conical.
5, as claim 1 or 3 described multistage inner circulation reactors, it is characterized in that: gas-liquid separator (80) is formed full circle shape at continuous bay wall.
6, as claim 1 or 3 described multistage inner circulation reactors, it is characterized in that: gas-liquid separator (80) is two semicircles, half connects odd number reaction zone upspout and return line (6), second half connects even number reaction zone upspout, after the up-flow gas-liquid of each reactor enters gas-liquid separator (80), biogas connects from the pipeline (9) of continuing to use of separator two halves, draws with valve switch (93) control, and gas meter (94) is set; Up-flow liquid is continued to use pipeline (61) and is communicated with under the two halves separator, return line (6) connects solid-liquid separator (70).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100696991A CN101293706B (en) | 2008-07-15 | 2008-07-15 | Multi-stage inner circulation anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100696991A CN101293706B (en) | 2008-07-15 | 2008-07-15 | Multi-stage inner circulation anaerobic reactor |
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| CN101293706A true CN101293706A (en) | 2008-10-29 |
| CN101293706B CN101293706B (en) | 2010-07-14 |
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| CN2008100696991A Expired - Fee Related CN101293706B (en) | 2008-07-15 | 2008-07-15 | Multi-stage inner circulation anaerobic reactor |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108609733A (en) * | 2018-06-12 | 2018-10-02 | 浙江大学 | IC anaerobic reactors slow down sludge calcification device and method |
| CN110028154A (en) * | 2019-05-08 | 2019-07-19 | 南京大学盐城环保技术与工程研究院 | It is a kind of without blocking water distribution anaerobic reaction device |
| CN110980943A (en) * | 2019-12-14 | 2020-04-10 | 浙江永续环境工程有限公司 | Anaerobic flowing biological membrane reactor |
| CN115340179A (en) * | 2022-05-27 | 2022-11-15 | 蚌埠市清泉环保有限责任公司 | Intelligence sewage anaerobic reactor |
-
2008
- 2008-07-15 CN CN2008100696991A patent/CN101293706B/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108609733A (en) * | 2018-06-12 | 2018-10-02 | 浙江大学 | IC anaerobic reactors slow down sludge calcification device and method |
| CN108609733B (en) * | 2018-06-12 | 2023-09-22 | 浙江大学 | Device and method for retarding sludge calcification by IC anaerobic reactor |
| CN110028154A (en) * | 2019-05-08 | 2019-07-19 | 南京大学盐城环保技术与工程研究院 | It is a kind of without blocking water distribution anaerobic reaction device |
| CN110028154B (en) * | 2019-05-08 | 2022-05-20 | 南京大学盐城环保技术与工程研究院 | Non-blocking water distribution anaerobic reaction device |
| CN110980943A (en) * | 2019-12-14 | 2020-04-10 | 浙江永续环境工程有限公司 | Anaerobic flowing biological membrane reactor |
| CN110980943B (en) * | 2019-12-14 | 2022-02-18 | 浙江永续环境工程有限公司 | Anaerobic flowing biological membrane reactor |
| CN115340179A (en) * | 2022-05-27 | 2022-11-15 | 蚌埠市清泉环保有限责任公司 | Intelligence sewage anaerobic reactor |
| CN115340179B (en) * | 2022-05-27 | 2023-08-15 | 蚌埠市清泉环保有限责任公司 | Intelligent sewage anaerobic reactor |
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| Publication number | Publication date |
|---|---|
| CN101293706B (en) | 2010-07-14 |
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Granted publication date: 20100714 Termination date: 20120715 |